Experimental and numerical study of free convective heat transfer in air performed simultaneously from the upper and lower surfaces of a horizontal plate heated on both sides

• The paper investigates convection from a double-sided heated horizontal plate • A new type of heating plate was designed and tested • Experimental and numerical analyses were conducted for both surfaces • Results show good correlation with numerical calculations for UWT and UHF conditions This paper presents an experimental study, supported by numerical analysis, on convective heat transfer in air from a newly designed, horizontal, double-sided heated Type II plate. Unlike the single-sided heated Type I plate, where the heating surface faces either upwards or downwards, the Type II plate heats both surfaces simultaneously. The tested plate was constructed from three glued laminates, each 0.6 mm thick, resulting in a total thickness of 2.1 mm. Minimal lateral-surface heat loss (<4.2%) ensured high measurement accuracy. Surface resistance thermometers ( T low/up ) were etched into the copper layer on one side, while two resistance heaters ( N low/up ) were embedded in the copper-coated middle laminate. Numerical calculations (Num.II and Num.I) for Type II and I plates revealed discrepancies under the UWT (Uniform Wall Temperature) condition: C Exp . II / C Num.II = 33.8% (upper) and -8.4% (lower), and for UHF (Uniform Heat Flux): 17.8% (upper) and 6.1% (lower). Similar discrepancies in C Num.II / C Num.I (-36.1% UWT up , 0.5% UWT low , -26.9% UHF up , 0.7% UHF low ) confirmed different heat transfer mechanisms on the upper heating surfaces of Type II and I plates. In the absence of the mean literature correlation (MLC.II) for Type II plates, numerical verification ( C Num.II ) was conducted, yielding C Exp. / C Num.II = 1.338 (upper) and 0.916 (lower) for UWT, and 1.178 (upper) and 1.061 (lower) for UHF. Indirect verification using Type I plate data (MLC.I) required numerical transformation, yielding C Exp.II / C MLC.I = 1.426 (upper) and 0.748 (lower) for UWT, and 1.017 (upper) and 0.896 (lower) for UHF. These results confirm the reliability of the Type II plate tests.

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Publication Details

Journal
International Journal of Heat and Mass Transfer
Published
2025-03-29
DOI
https://doi.org/10.1016/j.ijheatmasstransfer.2025.126973
Citations
3
Primary Topic
Heat Transfer and Optimization
Type
article
Field-Weighted Citation Impact
2.14
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article

Experimental and numerical study of free convective heat transfer in air performed simultaneously from the upper and lower surfaces of a horizontal plate heated on both sides

Michał Ryms, K. Tesch, Witold s.M. Lewandowski
3 citations
International Journal of Heat and Mass Transfer
Heat Transfer and Optimization
2.14
article

Experimental and numerical study of free convective heat transfer in air performed simultaneously from the upper and lower surfaces of a horizontal plate heated on both sides

Michał Ryms, K. Tesch, Witold s.M. Lewandowski
article en
3 citations

Abstract

• The paper investigates convection from a double-sided heated horizontal plate • A new type of heating plate was designed and tested • Experimental and numerical analyses were conducted for both surfaces • Results show good correlation with numerical calculations for UWT and UHF conditions This paper presents an experimental study, supported by numerical analysis, on convective heat transfer in air from a newly designed, horizontal, double-sided heated Type II plate. Unlike the single-sided heated Type I plate, where the heating surface faces either upwards or downwards, the Type II plate heats both surfaces simultaneously. The tested plate was constructed from three glued laminates, each 0.6 mm thick, resulting in a total thickness of 2.1 mm. Minimal lateral-surface heat loss (<4.2%) ensured high measurement accuracy. Surface resistance thermometers ( T low/up ) were etched into the copper layer on one side, while two resistance heaters ( N low/up ) were embedded in the copper-coated middle laminate. Numerical calculations (Num.II and Num.I) for Type II and I plates revealed discrepancies under the UWT (Uniform Wall Temperature) condition: C Exp . II / C Num.II = 33.8% (upper) and -8.4% (lower), and for UHF (Uniform Heat Flux): 17.8% (upper) and 6.1% (lower). Similar discrepancies in C Num.II / C Num.I (-36.1% UWT up , 0.5% UWT low , -26.9% UHF up , 0.7% UHF low ) confirmed different heat transfer mechanisms on the upper heating surfaces of Type II and I plates. In the absence of the mean literature correlation (MLC.II) for Type II plates, numerical verification ( C Num.II ) was conducted, yielding C Exp. / C Num.II = 1.338 (upper) and 0.916 (lower) for UWT, and 1.178 (upper) and 1.061 (lower) for UHF. Indirect verification using Type I plate data (MLC.I) required numerical transformation, yielding C Exp.II / C MLC.I = 1.426 (upper) and 0.748 (lower) for UWT, and 1.017 (upper) and 0.896 (lower) for UHF. These results confirm the reliability of the Type II plate tests.

International Journal of Heat and Mass TransferVol. 245
Gdańsk University of Technology (PL)
Openalex Percentile: Top 15%
Heat Transfer and Optimization
2.14
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